CN206985955U - Pharmacy wastewater treatment system - Google Patents
Pharmacy wastewater treatment system Download PDFInfo
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- CN206985955U CN206985955U CN201720484447.XU CN201720484447U CN206985955U CN 206985955 U CN206985955 U CN 206985955U CN 201720484447 U CN201720484447 U CN 201720484447U CN 206985955 U CN206985955 U CN 206985955U
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- CN
- China
- Prior art keywords
- pond
- tank
- waste water
- medicine storing
- pharmacy
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- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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- 238000004065 wastewater treatment Methods 0.000 title claims abstract description 19
- 239000002351 wastewater Substances 0.000 claims abstract description 45
- 238000004062 sedimentation Methods 0.000 claims abstract description 22
- 238000007254 oxidation reaction Methods 0.000 claims abstract description 20
- 230000003647 oxidation Effects 0.000 claims abstract description 19
- 238000005188 flotation Methods 0.000 claims abstract description 15
- 239000010865 sewage Substances 0.000 claims abstract description 14
- 230000007062 hydrolysis Effects 0.000 claims abstract description 12
- 238000006460 hydrolysis reaction Methods 0.000 claims abstract description 12
- 230000020477 pH reduction Effects 0.000 claims abstract description 12
- 238000012544 monitoring process Methods 0.000 claims abstract description 8
- 238000006243 chemical reaction Methods 0.000 claims abstract description 7
- 230000015271 coagulation Effects 0.000 claims abstract description 7
- 238000005345 coagulation Methods 0.000 claims abstract description 7
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 claims abstract description 5
- 239000003814 drug Substances 0.000 claims description 38
- 239000010802 sludge Substances 0.000 claims description 19
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 7
- 239000007788 liquid Substances 0.000 claims description 3
- 230000001105 regulatory effect Effects 0.000 claims description 3
- 238000003860 storage Methods 0.000 claims description 3
- 239000006228 supernatant Substances 0.000 claims description 3
- 239000002699 waste material Substances 0.000 claims description 3
- 229940079593 drug Drugs 0.000 claims description 2
- 230000014759 maintenance of location Effects 0.000 claims description 2
- 230000001112 coagulating effect Effects 0.000 claims 1
- 230000000694 effects Effects 0.000 abstract description 9
- 238000004519 manufacturing process Methods 0.000 abstract description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 7
- 238000012545 processing Methods 0.000 abstract description 3
- 230000003115 biocidal effect Effects 0.000 description 4
- 241000894006 Bacteria Species 0.000 description 3
- 238000000034 method Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000002574 poison Substances 0.000 description 2
- 231100000614 poison Toxicity 0.000 description 2
- 230000006978 adaptation Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000033228 biological regulation Effects 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000011010 flushing procedure Methods 0.000 description 1
- 238000009472 formulation Methods 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Landscapes
- Separation Of Suspended Particles By Flocculating Agents (AREA)
- Activated Sludge Processes (AREA)
Abstract
It the utility model is related to a kind of pharmacy wastewater treatment system, the side wall of grid pond is provided with pharmacy waste water water inlet pipe, grid pond is connected with collecting-tank, collecting-tank is connected by elevator pump with wastewater equalization pond, waste water lifting machine in wastewater equalization pond is connected with the shallow layer flotation machine being located on wastewater equalization pond, shallow layer flotation machine is connected by sewage conduct with ABR hydrolysis acidification pools, ABR hydrolysis acidification pools are connected by biological contact oxidation pond I with intermediate sedimentation pond, intermediate sedimentation pond is connected by the sewage conduct of side with biological contact oxidation pond II, biological contact oxidation pond II is connected by coagulation reaction tank with rectangular sedimentation tank, rectangular sedimentation tank is connected with monitoring well, COD devices are provided with monitoring well；Small volume, power consumption is low, operating cost bottom, good energy-conserving effect, good waste water treatment effect, and operating efficiency is high, reduces production cost, and reaches flexible operation, change that is easy to operate, adapting to water quality, water, it is ensured that stable effluent quality after processing, qualified discharge.
Description
Technical field
It the utility model is related to a kind of pharmacy wastewater treatment system.
Background technology
Pharmacy waste water mainly includes antibiotic production wastewater, synthetic drug production waste water, Chinese patent medicine production wastewater and each
The washings and the major class of flushing waste water four of class formulation manufacturing processes.The characteristics of its waste water is complicated component, content of organics height, poison
Property big, colourity depth and salt content it is high, particularly biochemical is very poor, and intermittent discharge, belongs to intractable industrial wastewater.With China
The development of medical industry, pharmacy waste water have been increasingly becoming one of important pollution sources.
Existing pharmacy waste water is typically handled using biochemical degradation method, however, containing the organic matters such as antibiotic poison
The pharmacy waste water of element, antibiotic therein has dissipation effect to biological bacteria, may refrain from biological bacteria flourish, so as to cause
Waste water containing antibiotic is difficult to be degraded by the method for the biological bacteria of routine, how to handle such waste water and becomes as current environment
One problem of protection.
Utility model content
The technical problems to be solved in the utility model is：Overcome deficiency in the prior art, there is provided a kind of good energy-conserving effect,
Good waste water treatment effect, operating efficiency is high, reduces production cost, and reach the pharmacy wastewater treatment system of flexible operation.
Technical scheme is used by the utility model solves its technical problem：A kind of pharmacy wastewater treatment system, has
Grid pond, medicine system and sludge concentration tank, the side wall of grid pond are provided with pharmacy waste water water inlet pipe, grid pond and collecting-tank
Connection, collecting-tank are connected by elevator pump with wastewater equalization pond, and the waste water lifting machine in wastewater equalization pond is with being located at waste water regulation
Shallow layer flotation machine connection on pond, shallow layer flotation machine are connected by sewage conduct with ABR hydrolysis acidification pools, ABR hydrolysis acidification pools
It is connected by biological contact oxidation pond I with intermediate sedimentation pond, the sewage conduct and biological contact oxidation that intermediate sedimentation pond passes through side
Change pond II to connect, biological contact oxidation pond II is connected by coagulation reaction tank with rectangular sedimentation tank, rectangular sedimentation tank and prison
Well logging connection, monitoring well is interior to be provided with COD devices；
The shallow layer flotation machine is connected by sludge pipe with sludge concentration tank, the ABR hydrolysis acidification pools, intermediate sedimentation pond
And the bottom of rectangular sedimentation tank is equipped with sludge pipe and is connected with sludge concentration tank, a side of the sludge concentration tank is provided with
Supernatant is connected by pipeline with wastewater equalization pond, and its bottom is connected provided with pipeline with pneumatic diaphragm pump, pneumatic diaphragm pump and van-type
Filter press connects.
Further, described medicine system includes PAC medicine storing pots, PAM medicine storing pots, NAOH medicine storing pots and standby storage
Medicinal cupping, the pipeline of the waste water lifting machine are connected with PAC medicine storing pots and PAM medicine storing pots, the pipeline of the shallow layer flotation machine with
NAOH medicine storing pots are connected, and the coagulation reaction tank is connected with PAC medicine storing pots and PAM medicine storing pots.
Further, it is provided with grid in described grid pond.
Further, it is equipped with described wastewater equalization pond, biological contact oxidation pond I and biological contact oxidation pond II
Air hose is connected with air blower.
Further, the side of described Waste Water Treatment is provided with accident pool, and measuring pump and sewage are provided with accident pool
Waste liquid is quantified, is uniformly sent into wastewater equalization pond by pipeline, sewage conduct.
The beneficial effects of the utility model are：The utility model small volume, power consumption is low, operating cost bottom, good energy-conserving effect,
Good waste water treatment effect, operating efficiency is high, reduces production cost, and reaches flexible operation, easy to operate, adaptation water quality, water
Change, it is ensured that stable effluent quality after processing, qualified discharge.
Brief description of the drawings
The utility model is further illustrated with embodiment below in conjunction with the accompanying drawings.
Fig. 1 is structural representation of the present utility model.
1. grid pond in figure, 2. medicine systems, 3. sludge concentration tanks, 4. pharmacy waste water water inlet pipes, 5. collecting-tanks, 6. waste water
Regulating reservoir, 7. shallow layer flotation machines, 8.ABR hydrolysis acidification pools, 9. waste water lifting machines, 10. biological contact oxidation ponds I, 11. centres are heavy
Shallow lake pond, 12. biological contact oxidation ponds II, 13. coagulation reaction tanks, 14. rectangular sedimentation tanks, 15. monitoring wells, 16.COD devices,
17. pneumatic diaphragm pump, 18. chamber-type press filters, 19.PAC medicine storing pots, 20.PAM medicine storing pots, 21.NAOH medicine storing pots, 22. standby storages
Medicinal cupping, 23. air blowers, 24. accident pools, 25. measuring pumps.
Embodiment
The utility model is further described presently in connection with accompanying drawing.These accompanying drawings are simplified schematic diagram only to show
Meaning mode illustrates basic structure of the present utility model, therefore it only shows the composition relevant with the utility model.
A kind of pharmacy wastewater treatment system as shown in Figure 1, has grid pond 1, medicine system 2 and sludge concentration tank 3,
The side wall of grid pond 1 is provided with pharmacy waste water water inlet pipe 4, and grid pond 1 is connected with collecting-tank 5, and collecting-tank 5 is by elevator pump with giving up
Water regulating reservoir 6 is connected, and the waste water lifting machine 9 in wastewater equalization pond 6 is connected with the shallow layer flotation machine 7 being located on wastewater equalization pond 6,
Shallow layer flotation machine 7 is connected by sewage conduct with ABR hydrolysis acidification pools 8, and ABR hydrolysis acidification pools 8 pass through biological contact oxidation pond I
10 are connected with intermediate sedimentation pond 11, and intermediate sedimentation pond 11 is connected by the sewage conduct of side with biological contact oxidation pond II 12,
Biological contact oxidation pond II 12 is connected by coagulation reaction tank 13 with rectangular sedimentation tank 14, rectangular sedimentation tank 14 and monitoring well
15 connections, monitoring well 15 is interior to be provided with COD devices 16；
The shallow layer flotation machine 7 is connected by sludge pipe with sludge concentration tank 3, and the ABR hydrolysis acidification pools 8, centre are heavy
Shallow lake pond 11 and the bottom of rectangular sedimentation tank 14 are equipped with sludge pipe and are connected with sludge concentration tank 3, the sludge concentration tank 3
Supernatant is connected by one side provided with pipeline with wastewater equalization pond 6, and its bottom is connected provided with pipeline with pneumatic diaphragm pump 17, pneumatically
Membrane pump 17 is connected with chamber-type press filter 18.
Medicine system 2 includes PAC medicine storing pots 19, PAM medicine storing pots 20, NAOH medicine storing pots 21 and standby medicine storing pot 22,
The pipeline of the waste water lifting machine 9 is connected with PAC medicine storing pots 19 and PAM medicine storing pots 20, the pipeline of the shallow layer flotation machine 7 with
NAOH medicine storing pots 21 are connected, and the coagulation reaction tank 13 is connected with PAC medicine storing pots 19 and PAM medicine storing pots 20.
Grid, wastewater equalization pond 6, biological contact oxidation pond I 10 and biological contact oxidation pond II 12 are provided with grid pond 1
Inside it is equipped with air hose to be connected with air blower 23, the side of Waste Water Treatment is provided with accident pool 24, and meter is provided with accident pool 24
Pump 25 and sewage conduct are measured, waste liquid is quantified, is uniformly sent into wastewater equalization pond 6 by sewage conduct, while small volume, power consumption
Low, operating cost bottom, good energy-conserving effect, good waste water treatment effect, operating efficiency is high, reduces production cost, and reaches operation spirit
Change that is living, easy to operate, adapting to water quality, water, it is ensured that stable effluent quality after processing, qualified discharge.
For above-mentioned embodiment only to illustrate technical concepts and features of the present utility model, its object is to allow be familiar with this skill
The personage of art can understand content of the present utility model and be carried out, and protection model of the present utility model can not be limited with this
Enclose, all equivalent change or modifications made according to the utility model Spirit Essence, should all cover in protection model of the present utility model
In enclosing.
Claims (5)
1. a kind of pharmacy wastewater treatment system, there is grid pond (1), medicine system (2) and sludge concentration tank (3), its feature
It is：The side wall of described grid pond (1) is provided with pharmacy waste water water inlet pipe (4), and grid pond (1) is connected with collecting-tank (5), collection
Pond (5) is connected by elevator pump with wastewater equalization pond (6), and the waste water lifting machine (9) in wastewater equalization pond (6) is with being located at waste water
Shallow layer flotation machine (7) connection on regulating reservoir (6), shallow layer flotation machine (7) are connected by sewage conduct and ABR hydrolysis acidification pools (8)
Connect, ABR hydrolysis acidification pools (8) are connected by biological contact oxidation pond I (10) with intermediate sedimentation pond (11), intermediate sedimentation pond (11)
It is connected by the sewage conduct of side with biological contact oxidation pond II (12), biological contact oxidation pond II (12) passes through coagulating
Pond (13) is connected with rectangular sedimentation tank (14), and rectangular sedimentation tank (14) is connected with monitoring well (15), is set in monitoring well (15)
There are COD devices (16)；
The shallow layer flotation machine (7) is connected by sludge pipe with sludge concentration tank (3), the ABR hydrolysis acidification pools (8), centre
The bottom of sedimentation basin (11) and rectangular sedimentation tank (14) is equipped with sludge pipe and is connected with sludge concentration tank (3), the sludge
Supernatant is connected by one side of concentration basin (3) provided with pipeline with wastewater equalization pond (6), and its bottom is provided with pipeline and pneumatic diaphragm
Pump (17) is connected, and pneumatic diaphragm pump (17) is connected with chamber-type press filter (18).
2. pharmacy wastewater treatment system according to claim 1, it is characterised in that：Described medicine system (2) includes
PAC medicine storing pots (19), PAM medicine storing pots (20), NAOH medicine storing pots (21) and standby medicine storing pot (22), the waste water lifting machine
(9) pipeline is connected with PAC medicine storing pots (19) and PAM medicine storing pots (20), pipeline and the NAOH drug storages of the shallow layer flotation machine (7)
Tank (21) connects, and the coagulation reaction tank (13) is connected with PAC medicine storing pots (19) and PAM medicine storing pots (20).
3. pharmacy wastewater treatment system according to claim 1, it is characterised in that：Lattice are provided with described grid pond (1)
Grid.
4. pharmacy wastewater treatment system according to claim 1, it is characterised in that：Described wastewater equalization pond (6), biology
Air hose is equipped with contact-oxidation pool I (10) and biological contact oxidation pond II (12) to be connected with air blower (23).
5. pharmacy wastewater treatment system according to claim 1, it is characterised in that：The side of described Waste Water Treatment
Provided with accident pool (24), measuring pump (25) and sewage conduct are provided with accident pool (24), sewage conduct quantifies waste liquid, uniformly
It is sent into wastewater equalization pond (6).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720484447.XU CN206985955U (en) | 2017-05-03 | 2017-05-03 | Pharmacy wastewater treatment system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720484447.XU CN206985955U (en) | 2017-05-03 | 2017-05-03 | Pharmacy wastewater treatment system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206985955U true CN206985955U (en) | 2018-02-09 |
Family
ID=61392629
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720484447.XU Active CN206985955U (en) | 2017-05-03 | 2017-05-03 | Pharmacy wastewater treatment system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206985955U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108467153A (en) * | 2018-05-02 | 2018-08-31 | 江苏大彭环保科技有限公司 | A kind of pharmaceutical wastewater treatment process |
| CN109264927A (en) * | 2018-10-10 | 2019-01-25 | 江苏开放大学（江苏城市职业学院） | A kind of processing unit and method of pharmaceutical wastewater |
| CN112851015A (en) * | 2020-12-21 | 2021-05-28 | 广州博才环保技术有限公司 | Chinese patent medicine wastewater treatment process and application method |
-
2017
- 2017-05-03 CN CN201720484447.XU patent/CN206985955U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108467153A (en) * | 2018-05-02 | 2018-08-31 | 江苏大彭环保科技有限公司 | A kind of pharmaceutical wastewater treatment process |
| CN109264927A (en) * | 2018-10-10 | 2019-01-25 | 江苏开放大学（江苏城市职业学院） | A kind of processing unit and method of pharmaceutical wastewater |
| CN112851015A (en) * | 2020-12-21 | 2021-05-28 | 广州博才环保技术有限公司 | Chinese patent medicine wastewater treatment process and application method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20190527 Address after: 626000 No. 123 East Street, Lucheng Town, Kangding City, Ganzi Tibetan Autonomous Prefecture, Sichuan Province Patentee after: Sichuan West Construction Engineering Co., Ltd. Address before: 214500 Tiancheng international 8F806, Jingping Road, Jingcheng street, Jingjiang, Taizhou, Jiangsu, China, 222 Patentee before: Huang Yingzhi |
|
| TR01 | Transfer of patent right |